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United States Patent |
5,614,103
|
Agree
,   et al.
|
March 25, 1997
|
Methods for detackifying paint spray booth water
Abstract
A method and composition for detackifying or coagulating and flocculating
waterborne and mixed waterborne/solventborne paints in paint spray booth
water. Aluminum chlorohydrate and a tannin containing polymer, preferably
in an aqueous solution, are added to the paint spray booth water to
detackify or coagulate and flocculate the paints.
Inventors:
|
Agree; Howard B. (Newtown, PA);
Chen; Jen-Chi (Morrisville, PA);
Iezzi; Robert A. (Malvern, PA)
|
Assignee:
|
BetzDearborn, Inc. (Trevose, PA)
|
Appl. No.:
|
354690 |
Filed:
|
December 13, 1994 |
Current U.S. Class: |
210/725; 210/728; 210/730; 210/734; 210/930; 524/437; 527/400 |
Intern'l Class: |
B01D 021/01 |
Field of Search: |
210/725,728,730,734,930
524/437,444,500
527/400
|
References Cited
U.S. Patent Documents
3861887 | Jan., 1976 | Forney | 55/19.
|
4637824 | Jan., 1987 | Pominville | 55/85.
|
4948513 | Aug., 1990 | Mitchell | 210/705.
|
5073205 | Dec., 1991 | Morse | 134/38.
|
5076939 | Dec., 1991 | Hunter et al. | 210/712.
|
5250189 | Oct., 1993 | Rey | 210/712.
|
5294352 | Mar., 1994 | Waldmann | 524/437.
|
Foreign Patent Documents |
0525989 | Jun., 1992 | EP.
| |
Primary Examiner: Reddick; Judy M.
Attorney, Agent or Firm: Ricci; Alexander D., Von Neida; Philip H.
Parent Case Text
This is a continuation-in-part of Ser. No. 08/246,547, May 20, 1994,
pending which is a continuation-in-part of Ser. No. 08/080,909, Jun. 22,
1993 now abandoned.
Claims
Having thus described the invention, what we claim is:
1. A method for detackifying or coagulating and flocculating waterborne and
mixed waterborne/solventborne paints in paint spray booth water comprising
adding to said paint spray booth water an effective detackifying or
coagulating and flocculating amount of a composition comprising a water
soluble or dispersible copolymer of tannin and a cationic monomer and
aluminum chlorohydrate.
2. The method as claimed in claim 1 wherein said composition comprises 10
to 90 weight percent of said copolymer and 90 to 10 weight percent of said
aluminum chlorohydrate based upon the total weight of said composition.
3. The method as claimed in claim 1 wherein said composition further
comprises water.
4. The method as claimed in claim 1 wherein said copolymer comprises 20 to
80 weight percent tannin and 80 to 20 weight percent cationic monomer
provided the total weight percent of said tannin and said cationic monomer
totals 100 weight percent.
5. The method as claimed in claim 1 wherein said copolymer comprises 30 to
50 weight percent tannin and 50 to 70 weight percent cationic monomer
provided the total weight percent of said tannin and said cationic monomer
totals 100 weight percent.
6. The method as claimed in claim 1 wherein said cationic monomer is
selected from the group consisting of methyl chloride or dimethyl sulfate
quaternary salt of dimethylaminoethyl acrylate, diethylaminoethyl
acrylate, dimethylaminoethyl methacrylate, diethylaminoethyl methacrylate,
dimethylaminopropyl methacrylamide, dimethylaminopropyl acrylamide, and
diallyl dimethyl ammonium chloride.
7. The method as claimed in claim 6 wherein said cationic monomer is methyl
chloride quaternary salt of dimethylaminoethyl acrylate.
8. The method as claimed in claim 1 wherein said tannin is Mimosa tannin.
9. The method as claimed in claim 1 wherein said composition is added to
said paint spray booth water in an amount ranging from 100 parts to about
2000 parts per million parts paint spray booth water.
10. The method as claimed in claim 1 wherein said paint spray booth water
has a pH of from 7 to about 9.
11. The method as claimed in claim 1 wherein said paints are selected from
the group consisting of polyacrylic, polyurethane, epoxy, and polyester
resin based paints.
Description
FIELD OF THE INVENTION
The present invention relates to methods for detackifying or coagulating
and flocculating waterborne and mixed waterborne/solventborne paints in
paint spray booth waters employing a composition of a tannin containing
polymer and aluminum chlorohydrate.
BACKGROUND OF THE INVENTION
The spray painting of automobile bodies, truck parts, appliances and other
industrial goods is typically carried out in enclosed areas called paint
spray booths (PSBs). These booths act to contain solvent fumes and
oversprayed paint and reduce the chances of dust contamination in order to
protect the paint booth operators and the painted articles. These booths
vary in size, but are somewhat basic in their design and operation. A
typical booth would thus consist of a work area, back section with mist
eliminators and a sump.
The articles to be painted generally pass through the work area while an
air flow makes overspray contact either water in the sump or spray from a
water curtain. The air is scrubbed with recirculated water at the water
curtain, passes through mist eliminators and is removed by an exhaust fan.
Even though paint transfer efficiencies have increased through improved
application technologies, roughly one-half of all paint sprayed does not
reach its intended article. As a result, significant concentrations of
paint buildup in the system and agglomeration can occur. When solventborne
paints are used, the resultant mass is a sticky, tacky material which can
plug mist eliminators, shower heads, and even recirculating pumps. When
waterborne paints are employed, they will remain dispersed in the spray
booth water. When present, waterborne paints will not present the same
problems as untreated solventborne paint (i.e., tackiness, clumps, etc.).
However, failure to remove waterborne paints results in increasing COD
(carbon oxygen demand) levels, increasing suspended solids, and increasing
levels of foam. All of these conditions decrease water clarity.
When water quality decreases, scrubbing efficiency decreases leading to
potentially hazardous conditions of unchecked paint emissions being
discharged into the atmosphere. Such conditions may also present severe
safety hazards to paint spray booth operators. The paint solids that are
collected in the water can form suspensions which remain tacky and create
expensive separation and disposal problems.
It is therefore desirable to treat paint spray booth water systems so as to
reduce or prevent, as much as possible, the agglomeration and deposition
of oversprayed paint on critical paint spray booth operating pads, to
render the resultant sludge (in solventborne systems) non-tacky and easily
removable, and to provide a water quality such that it can be recycled for
use in the system.
The paint employed in typical paint spray booths fall into two generic
classes, waterborne and solventborne. Currently, solventborne paints are
predominant. However, increased restrictions upon the levels of volatile
organic compound emissions are forcing industrial applications to switch
to waterborne paints.
The differences in the two paint classifications can be found in their
formulations. Solventborne paint typically consists of organic solvents
(such as xylene), resin binders, pigments and additives. In waterborne
systems, water is substituted for the organic solvent. Thus, the resin
binders, pigments, and additives must all be rendered water soluble or
dispersible. Resins which are not water soluble can be stabilized with
emulsifiers and cosolvents or be reformulated.
The behavior of a solventborne and a waterborne paint will differ when each
becomes overspray in a wet paint spray booth. Waterborne paints will
disperse in the aqueous medium, while solventborne paints agglomerate into
a tacky mass and adhere to paint spray booth operating pads. Because of
this behavior in water, in the past, the chemical process by which each
paint type is treated differs. In order to remove waterborne paint from an
aqueous medium, they should be considered as hydrophilic colloids which
must be rendered hydrophobic. The stability of the compounds in water
arises from the surface charge generated from carboxylic, aliphatic or
aromatic hydroxyl groups on the polymer backbone. The process of
destabilizing such solutions is termed coagulation. Flocculation follows
in this treatment process whereby the destabilized particles are induced
to come together, make contact and form large agglomerants.
Solventborne paints are hydrophobic and their treatment involves partially
dispersing the paint particles in the aqueous medium via an anionic
dispersant. The partially hydrophilic particles can then be treated to
render them non-tacky. This process is referred to as detackification.
SUMMARY OF THE INVENTION
The present invention relates to compositions of water soluble or
dispersible tannin containing polymers and aluminum chlorohydrate which
have been found to detackify solventborne paints and coagulate and
flocculate waterborne paints. The present invention is also effective at
treating mixed solventborne/waterborne paints.
DESCRIPTION OF THE RELATED ART
U.S. Pat. No. 4,948,513, Mitchell, teaches methods for detackifying spray
booth water containing paint particles by adding a combination of
hydrophilic/lipophilic quaternary ammonium repeat unit polymers or
diallyldialkyl quaternary ammonium compounds and the reaction product of
tannin, an amino compound and an aldehyde.
U.S. Pat. No. 5,073,205, Morse, teaches the use of copolymers of
N-methylolacrylamide and methyldiallylamine as detackifiers of
solventborne paints in the circulating water of water wash paint spray
booths. U.S. Pat. No. 5,250,189, Rey, teaches methods of treating paint
spray both water by maintaining the pH and alkalinity of the PSB water and
adding an aluminum salt and a flocculant to the water before contacting
the oversprayed, waterborne paint. The aluminum salt can be aluminum
chlorohydrate and the flocculant can be a cationic polyelectrolyte or
quaternary ammonium polymer. Hunter et al., U.S. Pat. No. 5,076,939,
teaches a method similar to Rey but substitutes an alumina coated silica
sol for the aluminum salt in the process.
U.S. Pat. No. 4,637,824, Pominville, teaches a method for detackifying
airborne paint particles captured in an aqueous wash stream by adjusting
the pH to 7 to 12 with an alkali metal silicate and then contacting the
paint wastes in the wash water with an amphoteric metal salt such as
aluminum chloride and a poly(diallyldimethyl ammonium halide) polymer.
EP 0 525 989A2, Huang et al., teaches a method for detackification of
oversprayed paint in wastewater by adding an amphoteric polymer and an
aluminum salt. The amphoteric polymer contains both anionic and cationic
mer units and preferably in the presence of (meth)acrylamide mer units.
DETAILED DESCRIPTION OF THE INVENTION
The present invention relates to a composition and methods for detackifying
or coagulating and flocculating waterborne and mixed
waterborne/solventborne paints in paint spray booth water comprising
adding to said paint spray booth water an effective amount of a water
soluble or dispersible tannin containing polymer and aluminum
chlorohydrate.
The tannin containing polymer comprises a water soluble or dispersible
polymer composition comprising a copolymer of tannin and a cationic
monomer. In another embodiment of the present invention, the tannin
containing polymer comprises a polymer of tannin and cationic monomer,
with at least one monomer selected from the group consisting of an anionic
monomer and a nonionic monomer.
The cationic monomer is selected from a group containing ethylenically
unsaturated quaternary ammonium, phosphonium or sulfonium ions. Typical
cationic monomers are quaternary ammonium salts of
dialkylaminoalkyl(meth)acrylamides, dialkylaminoalkyl(meth)acrylates and
diallyl dialkyl ammonium chloride.
The preferred cationic monomers are selected from the group include but are
not limited to methyl chloride quaternary salt of diethylaminoethyl
acrylate, dimethyl sulfate salt of diethylaminoethyl acrylate,
dimethylaminoethyl acrylate, dimethylaminoethyl methacrylate,
diethylaminoethyl methacrylate, dimethylaminopropyl methacrylamide,
dimethylaminopropyl acrylamide, diallyldimethyl ammonium chloride and
diallyldiethyl ammonium chloride. The most preferred cationic monomer is
methyl chloride quaternary salt of diethylaminoethyl acrylate.
The anionic monomer is selected from the group containing ethylenically
unsaturated carboxylic acid or sulfonic acid functional groups. These
monomers include but are not limited to acrylic acid, methacrylic acid,
vinyl acetic acid, itaconic acid, maleic acid, allylacetic acid, styrene
sulfonic acid, 2-acrylamido-2-methyl propane sulfonic acid (AMPS.RTM.) and
3-allyloxy-2-hydroxypropane sulfonic acids and salts thereof. The
preferred anionic monomer is acrylic acid.
The nonionic monomer is selected from the group of ethylenically
unsaturated nonionic monomers which comprise but are not limited to
acrylamide, methacrylamide, N-methylolacrylamide, N,N-dimethyl-acrylamide;
lower alkyl (C.sub.1 -C.sub.6) esters including vinyl acetate, methyl
acrylate, ethyl acrylate, and methyl methacrylate; hydroxylated lower
alkyl (C.sub.1 -C.sub.6) esters including hydroxyethyl acrylate,
hydroxypropyl acrylate and hydroxyethyl methacrylate; allyl glycidyl
ether; and ethoxylated allyl ethers of polyethylene glycol, polypropylene
glycol and propoxylated acrylates. The preferred nonionic monomers are
allyl glycidyl ether and acrylamide.
The resulting tannin containing polymer contains from 10 to 80% by weight
of tannin, 20 to 90% by weight of cationic monomer, 0 to 30% by weight of
nonionic monomer and 0 to 20% by weight of anionic monomer, provided that
the resulting tannin containing polymer is still water soluble or
dispersible and the total weight % of cationic, nonionic and anionic
monomers and tannin adds up to 100%. Preferably, when the cationic monomer
and anionic monomer are present together in the tannin containing polymer,
the cationic monomer comprises a greater weight percentage than the
anionic monomer.
The preferred copolymer of tannin and cationic monomer contains 20 to 80
weight % of tannin. More preferably, the copolymer contains from 30 to 60
weight % of tannin and most preferably, from 30 to 50 weight % of the
tannin in the copolymer, provided the total weight of tannin and cationic
monomer totals 100 weight %. More preferably still, the copolymers have a
weight % of 30% tannin and 70% cationic monomer and 50% tannin and 50%
cationic monomer. These particular copolymers are most preferred when the
tannin is a Mimosa type tannin and the cationic monomer is methyl chloride
quaternary salt of dimethylaminoethyl acrylate.
The number average molecular weight of the resulting tannin containing
polymer is not critical, as it is still water soluble or dispersible. The
tannin containing polymers may be prepared by mixing the desired monomers
with tannin and initiating by a free radical initiator via solution,
precipitation or emulsion polymerization techniques. Conventional
initiators such as azo compounds, persulfates, peroxides and redox couples
may be used. The preferred initiators are 2,2'azobis(2-amidinopropane)
dihydrochloride, available as V-50 from Wako Chemicals and
t-butylhydroperoxide/sodium metabisulfite (t-BHP/NaMBS). These or other
initiators may be added at the end of polymerization to further react with
any residual monomers.
Chain transfer agents such as alcohol, amine, formic acid or mercapto
compounds may be used to regulate the molecular weight of the polymer. The
resulting polymer may be isolated by well known techniques including
precipitation, etc., or the polymer may simply be used in its aqueous
solution.
The reaction temperature is not critical and generally occurs between
20.degree. and 100.degree. C., preferably 40.degree. to 70.degree. C. The
pH of the reaction mixture is also not critical and is generally in the
range of 2.0 to 8.0. The resulting tannin containing polymers are
characterized by C-13 NMR, Brookfield viscosity and percent solids.
The combination of aluminum chlorohydrate and tannin containing polymer
ranges from 10% to 90% aluminum chlorohydrate and 90% to 10% tannin
containing polymer by weight. Preferably, the range of aluminum
chlorohydrate is from 35% to 45% and the range of tannin containing
polymer is from 35% to 45%, with the remainder, by weight, being water.
The preferred tannin containing polymer is a copolymer of tannin and
cationic monomer. The copolymer contains 20 to 80% by weight percent of
tannin and more preferably 30 to 50 weight percent tannin, with 30% tannin
most preferred.
The preferred cationic monomer is methyl chloride quaternary salt of
dimethylaminoethylacrylate and the preferred tannin is a Mimosa type
tannin. The preferred copolymer will contain 30% by weight of Mimosa
tannin and 70% by weight of methyl chloride salt of
dimethylaminoethylacrylate.
The composition of the present invention is generally made up in a suitable
solvent which is preferably water. The dosage of composition added to the
paint spray booth water to be treated ranges from 100 parts to about 2000
parts per million parts paint spray booth water. A dosage range of 500
parts to about 1000 parts per million parts paint spray booth water is
preferred.
A preferred composition termed Treatment "A" is 35% aluminum chlorohydrate,
35% tannin containing polymer, and 30% water. The tannin containing
polymer is a copolymer of 30% by weight Mimosa tannin and 70% by weight
methyl chloride quaternary salt of dimethylaminoethacrylate.
The compositions of the present invention provide good coagulation and
flocculation of waterborne paints when the pH of the paint spray booth
water is between 7 and 9. It has been found that a small amount of
cationic flotation polymer is occasionally necessary to float the
detackified paint solids. The pH of the paint spray booth water can be
adjusted to the proper range with a caustic such as NaOH and KOH. For
solventborne/waterborne paint mixes, a cationic flotation polymer is added
to float the detackified paint solids. Examples of suitable cationic
flotation polymers include but are not limited to polyacrylamides and
acrylamidel/20% methyl chloride quaternary salt of diethylaminoethyl
acrylate (AETAC).
The methods of the present invention can be enhanced by combining the
compositions of the present invention with compounds such as inorganic
bases, silicates, acids, and metal salts. Preferred examples include but
are not limited to sodium hydroxide, potassium hydroxide, sodium silicate,
hydrochloric acid, and aluminum chlorohydrate.
The compositions of the present invention have been found to be an
effective treatment of polyacrylic, polyurethane, epoxy, and polyester
resin based paints. These paint types can be further classified to include
latexes, enamels, lacquers and acrylics.
In order to more clearly illustrate this invention, the data set forth
below were developed. The following examples are included as being
illustrations of the invention and should not be construed as limiting the
scope thereof.
EXAMPLES
The overall performance of the treatment program of the present invention
is analyzed for characteristics: detackification, flocculation, and water
clarity. A standard jar test procedure is used to determine the functional
dosage levels and proper combinations of cationic polymer and inorganic
materials. The general procedure is to add 100 mL of tap water to a 120 mL
jar. The treatment program is added, and the bottle is capped and shaken
to mix the contents. One mL of an automotive paint (waterborne or
solventborne/waterborne paint, mix) is then added to the jar. After
vigorous shaking for 30 seconds, a wooden tongue depressor is immersed in
the solution and then removed for examination. The following guidelines
are used for examining the detackification performance of the treatment.
______________________________________
Rating Definition
______________________________________
1 Paint forms large tacky globules and/or coating which
adheres to the exposed surfaces of the jar and
tongue depressor.
2 Paint forms agglomerates which are slightly tacky to
the touch, or upon crushing. Paint sludge coats the
tongue depressor.
3 Paint forms granular flocs which adhere to less than
10% of the exposed surface of the jar or depressor.
Sludge may be smeary, but not tacky.
4 Paint forms particles, some of which appear as specs
on less than 1% of the exposed surface area of the
jar or depressor. Sludge is neither smeary nor tacky.
5 Paint forms particles which do not adhere to the
exposed surfaces of the jar or depressor. The paint
sludge may float, sink, or be dispersed in the water.
______________________________________
The treatment composition utilized in the testing is identified as
Treatment A which is 35% aluminum chlorohydrate, 35% tannin containing
polymer (copolymer of 30% by weight Mimosa tannin/70% by weight methyl
chloride quaternary salt of dimethylamino ethylacrylate) and 30% water.
The treatment is fed as a percent by weight, based on paint,
conventionally known in the art as BOP.
TABLE I
______________________________________
Standard Jar Test
Waterborne Paint
Water
Sample
Paint BOP Activator
Rating
Clarity
______________________________________
1 PPG (acrylic) 5% O 4+ Clear -
2 10% O 4+ Clear
3 General (polyacrylic)
10% O 4+ Cloudy
4 15% O 4+ Clear
5 JEMA (synthetic
10% O 4+ Cloudy
enamel)
6 15% O 4+ Clear
7 PPG (acrylic/epoxy)
10% O 4+ Clear -
8 15% O 4+ Cloudy
9 10% NaOH; 4+ Clear
pH = 9
______________________________________
The results of this testing indicate that the inventive composition
provided excellent paint detackification and coagulation/flocculation
while yielding very clear water.
TABLE II
______________________________________
Standard Jar Test
Solventborne/Waterborne Paint Mixes
Sample Paint BOP Activator Rating
______________________________________
1 A 10% O 3
2 A 10% NaOH; pH = 9 4
3 A 15% NaOH; pH = 9 4+
4 B 5% O 3
5 B 10% O 4+
6 C 10% O 4/4+
7 C 15% O 4/4+
8 C 10% NaOH; pH = 9 4+
9 D 15% O 4/4+
10 D 15% NaOH; pH = 9 4+
11 D 15% KOH (1200 ppm)
4+
12 D 15% Silicate (1600 ppm)
3
13 E 15% O 3+
14 E 10% KOH (1000 ppm)
4+
15 E 10% Silicate (1000 ppm)
4+
16 E 10% NaOH; pH = 9 4
______________________________________
Paint Codes:
A = BASF Melamine solventborne/PPG acrylic waterborne
B = BASF Urethane solventborne/BASF acrylic waterborne
C = BASF Urethane solventborne/PPG acrylic waterborne
D = PPG Melamine solventborne/JEMA clear synthetic waterborne
E = BASF Urethane solventborne/PPG acrylic waterborne
As the results of Table II demonstrate, excellent detackification of
solventborne/waterborne mixed paints was achieved by the inventive
compositions with and without NaOH, KOH or silicate.
TABLE III
______________________________________
Standard Jar Test
Waterborne Paints
Water
Sample
Paint BOP pH Rating
Clarity
______________________________________
1 PPG acrylic 5% 8.3
4+ Cloudy
2 10% 8.3
4+ Clear
3 10% 10 4+ Cloudy
4 10% 9 4+ Clear
5 10% 6 4+ Cloudy
6 10% 7 4+ Clear
7 JEMA Clear Synthetic
10% 8.1
4+ Cloudy
8 15% 8 4+ Cloudy
9 20% 8 4+ Clear
10 20% 6 4+ Clear -
11 20% 7 4+ Clear
12 20% 9 4+ Clear
13 20% 10 4+ Cloudy
14 PPG acrylic 10% 8.3
4+ Clear
15 10% 6 4+ Cloudy
16 10% 7 4+ Clear
17 10% 9 4+ Clear
______________________________________
This data again demonstrates the effectiveness of the inventive composition
at detackification, flocculation and flotation at various water pHs. This
also indicates its particular effectiveness in water with pH between 7 and
9 for waterborne paints.
The inventive compositions were tested with a GM waterborne paint in a
bench top spray booth. The preliminary jar tests indicated that the paint
could be detackified with 10% BOP/NaOH adjusted pH=9.0. The booth was
charged with 1000 ppm of Treatment A and adjusted with caustic to pH of
9.0. To simulate actual plant conditions, 500 ppm of MEK/DMEA solvent
blend was added to the paint water.
The Treatment A solution was added at a rate of 10% BOP. The GM waterborne
paint was sprayed at an average rate of 0.20 g/10 sec. Throughout the test
the paint detackification was excellent, and the solids were suspended. A
sample of the paint water was treated with 10 ppm of polymer 25 L and 100%
of the paint solids floated.
Another bench top spray booth test was performed utilizing the inventive
compositions with a CPC-OKC solventborne/VVindsor waterborne mixed paint.
The booth was charged with 1000 ppm of Treatment A and 1000 ppm of DETAC
831. To simulate actual plant conditions, 500 ppm of MEK/DMEA solvent
blend was added to the paint water.
Treatment A was then added at a rate of 10% BOP. The mixed
solventborne/waterborne paint was sprayed at an average rate of 0.22 g/10
sec. Throughout the 85 minute test, paint detackification was excellent
with very little foaming.
While this invention has been described with respect to particular
embodiments thereof, it is apparent that numerous other forms and
modifications of this invention will be obvious to those skilled in the
art. The appended claims and this invention generally should be construed
to cover all such obvious forms and modifications which are within the
true spirit and scope of the present invention.
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